DE602006006226D1 - METHOD FOR PRODUCING A CALIBRATED EMULSION - Google Patents

METHOD FOR PRODUCING A CALIBRATED EMULSION

Info

Publication number
DE602006006226D1
DE602006006226D1 DE602006006226T DE602006006226T DE602006006226D1 DE 602006006226 D1 DE602006006226 D1 DE 602006006226D1 DE 602006006226 T DE602006006226 T DE 602006006226T DE 602006006226 T DE602006006226 T DE 602006006226T DE 602006006226 D1 DE602006006226 D1 DE 602006006226D1
Authority
DE
Germany
Prior art keywords
phase
mixing
scraping
agitator
diluting
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Expired - Fee Related
Application number
DE602006006226T
Other languages
German (de)
Inventor
Jean-Philippe Gingras
Philippe A Tanguy
Louis Fradette
Eric Jorda
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
TotalEnergies SE
Original Assignee
Total SE
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Total SE filed Critical Total SE
Publication of DE602006006226D1 publication Critical patent/DE602006006226D1/en
Expired - Fee Related legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Classifications

    • C—CHEMISTRY; METALLURGY
    • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10L—FUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G, C10K; LIQUEFIED PETROLEUM GAS; ADDING MATERIALS TO FUELS OR FIRES TO REDUCE SMOKE OR UNDESIRABLE DEPOSITS OR TO FACILITATE SOOT REMOVAL; FIRELIGHTERS
    • C10L1/00—Liquid carbonaceous fuels
    • C10L1/32—Liquid carbonaceous fuels consisting of coal-oil suspensions or aqueous emulsions or oil emulsions
    • C10L1/328—Oil emulsions containing water or any other hydrophilic phase
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
    • B01F23/00—Mixing according to the phases to be mixed, e.g. dispersing or emulsifying
    • B01F23/40—Mixing liquids with liquids; Emulsifying
    • B01F23/41—Emulsifying
    • B01F23/4105—Methods of emulsifying
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
    • B01F23/00—Mixing according to the phases to be mixed, e.g. dispersing or emulsifying
    • B01F23/40—Mixing liquids with liquids; Emulsifying
    • B01F23/43—Mixing liquids with liquids; Emulsifying using driven stirrers
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
    • B01F27/00—Mixers with rotary stirring devices in fixed receptacles; Kneaders
    • B01F27/80—Mixers with rotary stirring devices in fixed receptacles; Kneaders with stirrers rotating about a substantially vertical axis
    • B01F27/84—Mixers with rotary stirring devices in fixed receptacles; Kneaders with stirrers rotating about a substantially vertical axis with two or more stirrers rotating at different speeds or in opposite directions about the same axis
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
    • B01F27/00—Mixers with rotary stirring devices in fixed receptacles; Kneaders
    • B01F27/80—Mixers with rotary stirring devices in fixed receptacles; Kneaders with stirrers rotating about a substantially vertical axis
    • B01F27/85—Mixers with rotary stirring devices in fixed receptacles; Kneaders with stirrers rotating about a substantially vertical axis with two or more stirrers on separate shafts

Landscapes

  • Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Engineering & Computer Science (AREA)
  • General Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Mixers Of The Rotary Stirring Type (AREA)
  • Colloid Chemistry (AREA)
  • Processes Of Treating Macromolecular Substances (AREA)
  • Cosmetics (AREA)
  • Agricultural Chemicals And Associated Chemicals (AREA)
  • Polymerisation Methods In General (AREA)

Abstract

The semi continuous preparation of emulsion droplets of phase A in phase B, comprises mixing the mixture of the phase A and the phase B by a mixing system having scraping agitators (3a, 3b) with coaxial multiple shafts (2a, 2b) to obtain a dispersion of phase A in phase B with a volume concentration of phase A higher than 74%, and diluting the dispersion by addition of the phase B through a mixing system with the coaxial multiple shafts to obtain the emulsion droplets of the phase A in the phase B. The mixing system with the coaxial multiple shafts has non-scraping agitator. The semi continuous preparation of emulsion droplets of phase A in phase B, comprises mixing the mixture of the phase A and the phase B by a mixing system having scraping agitators (3a, 3b) with coaxial multiple shafts (2a, 2b) to obtain a dispersion of phase A in phase B with a volume concentration of phase A higher than 74%, and diluting the dispersion by addition of the phase B through a mixing system with the coaxial multiple shafts to obtain the emulsion droplets of the phase A in the phase B. The mixing system with the coaxial multiple shafts has non-scraping agitator with a speed of =12 m/s at a time of mixing. The average diameter of the emulsion droplets is controlled by an adjustment of deformation applied at the time of the mixing. The mixing step is carried out at the rate of deformation of 5-150 s -> 1>. The agitator scraping is used at a speed of =2.5 m/s. The scraping and non-scraping agitator is in a rotation or a counter rotation form. A mean velocity of rotation of the scraping agitator is lower in the diluting step than the mixing step. A mean velocity of the non-scraping agitator is higher in the diluting step than the mixing step. The number of revolutions of the scraping agitator at diluting step is five times higher than the mixing step. The number of revolutions of the non-scraping agitator at diluting step is twice the mixing step. The average diameter of the emulsion droplet is lower than 1 micron. The emulsion droplet has polydispersity of lower than 0.2. The phase A is added to the phase B with a mass flow of 0.01 - 3 times mass of the phase B per second. The phase B is added to phase A with a mass flow of 0.0001 - 0.1 times mass of phase A per second in mixing step. The phase A is bitumen or aqueous solution and the phase B is a aqueous solution or bitumen.
DE602006006226T 2005-12-16 2006-12-15 METHOD FOR PRODUCING A CALIBRATED EMULSION Expired - Fee Related DE602006006226D1 (en)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
FR0512826A FR2894845B1 (en) 2005-12-16 2005-12-16 PROCESS FOR PREPARING A CALIBRATED EMULSION
PCT/FR2006/002757 WO2007074225A1 (en) 2005-12-16 2006-12-15 Method for preparing a calibrated emulsion

Publications (1)

Publication Number Publication Date
DE602006006226D1 true DE602006006226D1 (en) 2009-05-20

Family

ID=36975332

Family Applications (1)

Application Number Title Priority Date Filing Date
DE602006006226T Expired - Fee Related DE602006006226D1 (en) 2005-12-16 2006-12-15 METHOD FOR PRODUCING A CALIBRATED EMULSION

Country Status (8)

Country Link
US (1) US8267574B2 (en)
EP (1) EP1973636B1 (en)
AT (1) ATE427781T1 (en)
CA (1) CA2633388C (en)
DE (1) DE602006006226D1 (en)
ES (1) ES2324894T3 (en)
FR (1) FR2894845B1 (en)
WO (1) WO2007074225A1 (en)

Families Citing this family (15)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US8557588B2 (en) * 2007-03-27 2013-10-15 Schlumberger Technology Corporation Methods and apparatus for sampling and diluting concentrated emulsions
ES2343399B1 (en) * 2009-01-28 2011-06-17 Repsol Ypf, S.A CONTINUOUS PREPARATION PROCEDURE FOR BETUN SUBMICRONIC EMULSIONS.
IT1396114B1 (en) * 2009-09-23 2012-11-16 Samia S P A PLANT FOR THE PRODUCTION OF COMPOSITIONS, SUCH AS STUCKS, BINDERS AND THE LIKE, PARTICULARLY SUITABLE FOR USE IN THE TANNING INDUSTRY AND PROCEDURE FOR THE PRODUCTION OF SUCH COMPOSITIONS THROUGH SUCH A PLANT.
EP2319328B1 (en) * 2009-11-06 2014-09-03 Kraft Foods R & D, Inc. Process for tempering chocolate
JP5507212B2 (en) * 2009-11-13 2014-05-28 東レ・ダウコーニング株式会社 Method for producing oil composition containing silicone powder
JP5755474B2 (en) * 2011-03-23 2015-07-29 佐竹化学機械工業株式会社 Stirrer
FR2994189B1 (en) * 2012-08-02 2015-10-02 Colas Sa PROCESS FOR PREPARING A FINE BITUMINOUS BINDER EMULSION
US20190292486A1 (en) * 2016-07-08 2019-09-26 Castrol Limited Metalworking Fluid
EP3481929A1 (en) * 2016-07-08 2019-05-15 Castrol Limited Metalworking fluid
EP3481932A1 (en) * 2016-07-08 2019-05-15 Castrol Limited Industrial fluid
EP3481930A1 (en) * 2016-07-08 2019-05-15 Castrol Limited Industrial fluid
CN109126496A (en) * 2018-07-19 2019-01-04 宁波帝杨电子科技有限公司 A kind of emulsifying device for asphalt based on ultrasonic atomization
CN111530315A (en) * 2020-05-07 2020-08-14 青岛中加特电气股份有限公司 Method, equipment and storage medium for controlling concentration ratio of emulsion
CN111773957A (en) * 2020-06-16 2020-10-16 马鞍山采石矶涂料有限公司 Paint blending device for preventing wall adhesion
BE1030815B1 (en) * 2022-08-24 2024-03-25 Gb Foods Belgium N V METHOD FOR EMPTYING AND/OR CLEANING A MIXING CHAMBER FOR POWDERED FOODSTUFFS

Family Cites Families (19)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US1384805A (en) * 1920-03-05 1921-07-19 Francis R Mullin Process for emulsifying oil or asphalt
GB244135A (en) * 1924-06-10 1925-12-10 Lester Kirschbraun Process of and apparatus for making emulsions
US1916885A (en) * 1930-12-20 1933-07-04 Flintkote Co Process and apparatus for producing emulsions
US2928665A (en) * 1950-09-27 1960-03-15 American Instr Co Inc Gas-liquid mixing apparatus
FR1383201A (en) * 1963-11-25 1964-12-24 Apparatus for emulsifying bitumen and similar substances
US3669900A (en) * 1969-05-02 1972-06-13 Pacific Vegetable Oil Corp Method and apparatus for continuous production of oil-in-water emulsions
DE2757486A1 (en) * 1977-12-22 1979-07-05 Draiswerke Gmbh DEVICE FOR DISCONTINUOUS MIXING OF AT LEAST TWO SUBSTANCES
US4197019A (en) * 1979-01-11 1980-04-08 Schold George R Dual drive co-axial disperser
DE3027567A1 (en) * 1980-07-21 1982-02-25 Dieter 6570 Kirn Kupka AGITATOR WITH TWO AGITATING ORGANS DRIVED AROUND THE SAME GEOMETRIC AXIS
GB8410741D0 (en) * 1984-04-26 1984-05-31 British Petroleum Co Plc Emulsions
US5354504A (en) * 1991-08-19 1994-10-11 Intevep, S.A. Method of preparation of emulsions of viscous hydrocarbon in water which inhibits aging
CH682788A5 (en) * 1992-04-14 1993-11-30 Frisse Richard Maschf Machine for processing chocolate masses.
US5835174A (en) * 1995-10-12 1998-11-10 Rohm And Haas Company Droplets and particles containing liquid crystal and films and apparatus containing the same
US6037058A (en) * 1995-10-12 2000-03-14 Rohms And Haas Company Particles and droplets containing liquid domains and method for forming in an acueous medium
US5611619A (en) * 1996-06-27 1997-03-18 Li Yuan Machine Industrial Co., Ltd. Mixing machine
US6431742B2 (en) * 2000-07-31 2002-08-13 Dow Corning Toray Silicone Co., Ltd. Continuous mixing apparatus with upper and lower disk impellers each having scrapers
US6677387B2 (en) * 2002-06-03 2004-01-13 Intevep, S.A. Preparation of stable emulsion using dynamic or static mixers
GB0329178D0 (en) * 2003-12-17 2004-01-21 Ici Plc Surfactant
US20080242739A1 (en) * 2007-03-30 2008-10-02 Gijsbert Kroon Mixed hydrophobe polysaccharide as polymeric emulsifier and stabilizer

Also Published As

Publication number Publication date
ATE427781T1 (en) 2009-04-15
EP1973636B1 (en) 2009-04-08
EP1973636A1 (en) 2008-10-01
CA2633388A1 (en) 2007-07-05
FR2894845B1 (en) 2008-02-29
WO2007074225A1 (en) 2007-07-05
CA2633388C (en) 2012-12-04
ES2324894T3 (en) 2009-08-18
WO2007074225A8 (en) 2007-09-27
FR2894845A1 (en) 2007-06-22
US20080310252A1 (en) 2008-12-18
US8267574B2 (en) 2012-09-18

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Legal Events

Date Code Title Description
8364 No opposition during term of opposition
8339 Ceased/non-payment of the annual fee